US1343575A

US1343575A - Manufacture of phenolic condensation products

Info

Publication number: US1343575A
Application number: US281642A
Authority: US
Inventors: Clarence A Nash
Original assignee: Individual
Current assignee: Individual
Priority date: 1919-03-10
Filing date: 1919-03-10
Publication date: 1920-06-15
Anticipated expiration: 1937-06-15

Description

UNITED STATES PATENT OFFICE.

- CLARENCE A. NASH, OF MILWAUKEE, WISCONSIN.

MANUFACTURE OF PHENOLIC CONDENSATION PRODUCTS.

No Drawing.

To all whom it may concern:

Be it known that I, CLARENCE A. NASH, a citizen of the United. States, residing at Milwaukee, in the county of Milwaukee and State of Wisconsin, have invented a new and useful Improvement in Manufacture of Phenolic Condensation Products, of which the following is a specification;

The present invention is in the nature of an improvement upon the method of manufacturing phenolic condensation products described and claimed in the application of -L. V. Redman, A. J. Weith, and Frank P. Brock, filed of even date herewith.

As is known, a. phenolic condensation product is produced by combining a phenolic body, such as phenol or its homologues', with an active methylene substance, such as hexamethylenetetramin or formaldehyde, containing the methylene radical.

It is well known that a phenolic condensation product (usually having a filler introduced therein) may be molded in hot presses and discharged hot or cold,as desired. It has been proposed, also, to mix a phenolic condensation product with a filler and'mold the same in the regular manner of coldmolded products, the final hardening being effected by subjecting the molded articleto the action of heat after its removalfrom the mold. Thus, in patent to Hemming No.

' 1,125,906, granted January 19, 1915, it is proposed to prepare an initia'l"-"product of phenol and formaldehyd'efthe latter in decided excess); arrest the reaction when a soluble resin of sp. gr. of from 1.15 to 1.21 has been produced; mix this binder with a filler; and then mold the mixture ind harden by heat treatment. This calls for a reaction in the moldedproduct in which water is formed as a by-product and mustbe eliminated by heat, tending to the production of a spongy and otherwise inferior product. Moreover, difiiculty hasbeen experienced in securing resins ofproper consistency to permit the mass to be properly kneaded and afterward properly molded by a cold-molding process. This is due partly to. the volatile nature of formaldehyde, and the difliculty 'o f determining the loss of methylene. It has been firoposemhalso, to use such solvents as alco in anefi'ort to secure the proper consistency and t proper coherency'in the molding but this involves additional exthe -ployed as a binder corresponds with the.

ol, acetone, etc.,

Specification of Letters Patent. Patented J 11113 15 1920,. Application filed March 10, 1919. Serial No, 281,642.

and is otherwise objectionable, and especially so because of the difliculty of securing the resin in a stage of reaction at which it is best adapted for the purpose. Again, in

Hemming process, the initial resin emunion of a major part of the formaldehyde with the phenolic body, so that even a resin of the lowest specific gravity mentioned by him, viz. 1.15, corresponds with a reaction so far advanced that the resin will not properly impregnate the filler; and after the mixing action has occurred, the particles or pellets of the molding compound will not be properly welded together by a cold molding operation. Notwithstanding, therefore,.the great desirability of a quickmolding process adapted to the production of molded phenolic condensation product articles, no published or patented process has met the demand, and a quick-molding process for this class of product has not come into general use. The present invention is being successfully practised, and will meet a long-felt want.

-The primary object of the present invention is to provide an improved practicable methodwhereby molded phenolic condensation product articles may be produced by a quick-molding operation at ordinary or moderate temperatures, followed by heat treatment after removal from the mold, to

convert the molded article to a hard andsubstantially infusible state.

method, the output of the molds may be in-' By such .a

creased many fold. As an improvement upon the process described in the above-mentioned application,'the present process poss'esses the advantage that it may be practised with greater facility,.that it will result in an article of more uniform tensile strength and of maximum dielectric constant, and that it will result in an article possessing the maximum resistance to water absorption.

In the practice of the present invention, it is entirely feasible for a manufacturer of phenolic condensation products to supply to manufacturers ofmolded products a phenolic condensation .produ'ct suitable for use "in producing a molding compound adapted to a quick-molding process, followed by heat treatment to convert the molded article to p a hard, resistant and practically infusible state. Also, the improved process is fof a nature rendering it comparatively easy for a manufacturer of molded products to produce a phenolic condensation product moldingcompound Without the aid or employment of chemists who are especially skilled in the production of phenolic condensation products. Also, the improved process may be practised with thegreatest certainty of uniformity in results, without the exercise of any extraordinary care, as, for instance, in determining the stage at which the reaction is to be stopped in order to obtain an initial fusible condensation product which 7 ,ployed in making such product is combined with the phenolic body employed, such fusible product corresponding with the union of about 2.; phenolic groups to onemethylene group; add to the initial fusible product a sufficient quantity of a non-volatile methylene substance which is capable of combining anhydrously with the fusible condensation product to convert the product to a hard and substantially infusible state; add to a given weight of asbestos in a mixer about 2% by Weight of a slowly-volatile hydrocarbon solvent for the binder, such as creosote oil, or an oil obtained from the distillation of coal tar, or asphalt thoroughly knead or mix the asbestos with the hydrocarbon solvent, which may require a period of from ten minutes to thirty minutes; then pour into the asbestos thus impregnated with the hydrocarbon solvent about by weight of the potentially reactive binder prepared as indicated above, the binder be ing in molten condition and at a temperature of about 100 F. to 140" F.; and mix the mass thoroughly, which may require about one-half hour. In the mixing operation, the materials will form into balls and pellets, being in a more or less disintegrated condition. The materials are then preferably dried by passing warm air over the same, and during this operation, which may re quire from one to several days, the material undergoes a change which is partly physical and partly chemical. The material then is preferably broken up in a disinte'grator, until it is from B to 20 mesh, or finer. In this condition,.the material is suitable for a quick-molding operation, followed by heat treatment to convert the molded article,-

after removal from the mold, to a hard and substantially infusible state. The molding operation may be performed in a few seconds under a suitable pressure, as, for instance, from 5,000 pounds to 15,000 pounds per square inch. The molded article is sufficiently firm to withstand removal from the mold and subjection to the subsequent heat treatment. After removal from the molds, the molded articles are preferably cured in an oven at a temperature ranging from 100 F. to 450 F., the temperature being preferably raised from time to time as the curing operation proceeds. The heat treatment may vary, however, greatly, depending upon the nature of the molded article but in any event should be continued until the molded article is converted to a hard, resistant and substantially infusible state. \Vhere the filler employed is an inorganic filler, such as asbestos, the final temperature may range as high as 450 F. \Vhere an organic filler, such as wood flour, is employed, the highest temperature employed should not reach the point at which charring would occur. Where the molded article is of uniform thickness, it is practicable to introduce the molded article into an oven heated to 350 F. at the outset, and a cure may be effected in from fifteen minutes to three hours, depending upon the size and thickness of the article. Vhere the article has metal inserts, or has recesses in it with walls of varying thickness, the heat treatment must be more cautiously performed, and will require a greater length of time.

By mixing the filler in the first instance 'with a small quantity of a non-volatile solvent of the nature indicated above, the

filler can, with the greatest facility, be thoroughly and uniformly impregnated by the solvent, so that all of the fibers are moistened; and this has the effect of facilitating the mixture of the filler and the phenolic binder, with the result that all of. the fibers of the filler are finally impregnated by the phenolic binder. Thus, an intimate mixture of the filler and the binder is obtained; and so, when the molding operation is performed, a thorough welding of the granulated particles of the molding compound occurs, so that a truly integral mass results. Thus, there is produced by the quick-molding process an article of high tensile strength, high dielectric constant,

andlow water absorptive quality.

The use of a slowly-volatile solvent hava relatively high boiling point is desirable, both because of the increased spreading, diffusing, or impregnating quality which it gives to the binder, and also because the use of such solvent serves to keep the materials in proper condition for molding for a comparatively long period of time; and in the heat treatment, after the molding operation, the solvent having a high boiling point acts as a tempering agent, and will not be readily driven off. whereas more usual solvents, such as alcohol, acetone, or

drocarbon which cannot be designated by definite formula. 0

The heat treatment of the molded artlcles may be performed advantageously 1n a closed oven, kiln, or vulcanizer. Usually it is desirable to make provision for the escape and collection of the amnfonia which is given off during the baking operatlon. The ammonia may be collected and used again, for instance, in making a" fresh supply of hexamethylenetetramm. i

Any suitable filler, such as asbestos, mlca, flock, wood pulp, etc., may be employed.

It is desirable to use, ordinarily, a high proportion of filler. In the case of asbestos, an excellent product is obtained by using to 80% by weight of asbestos and 20% to 40% by weight of binder. The proportions may vary greatly, however. It is desirable, both for economy and facility in producing a molding compound adapted to the quick-molding process, to employ a high percentage of filler. In the case of wood flour, the filler and binder may be advantageously of about equal weights. Proportions of the fusible condensation product and the methylene body em loyed may vary somewhat, 'but it is desira le to have approximately one methylene group to each phenolic group in the final product.

The use of a solvent of the character referred to above imparts to the molding compound a quality which prevents injury to the dies in the molding operation, so that the sharp edges or corners of the dies will not wear off, and it is thus possible to preserve sharp outlines in the molded product for a very large number of operations. This is a very important consideration, and the result is doubtless due to the fact that the great body of molding compound retains the solvent, even after there has been an apparent surface evaporation from the particles, or pellets, which make up the compound, so that the compound retains perfect plasticity and will not out the dies, even though the molding operation be not performed until a COIlSlCl QIELblG time after the compound has been prepared. I

As ystated, the fusible substantially anhydrous phenolic condensation product which it is preferred to employ as the main part methylenetetramim.

tetramin to 14 mols of phenolic groups of the binder preferably containsabout 2J2 phenolic groups to each methylene group. This may vary, however, from a lower limit of about two phenolic groups to each methylene group to an upper limit of aboutthree and one-half phenolic groups to each methylene group. It is not desirable in practice, however, to employ less than 2% phenolic groups to each methylene group, or to employ more than 3 phenolic groups to'each methylene group. Where the methylene body employed in preparing the fusible phenolic condensation product is hexathe ration of 2% phenolic groups to one methylene group correspondswith about one mol of hexam'ethylenetetramin to fourteen mols of cresol.

The fusible substantially binder which it is preferred to employ in the practice of the process is produced preferably by either of the two methods which follow, viz.:

8% Mix 1080 pounds of cresol (2 C H OH) and 140 ounds of hexamethylenetetramin (CH heat themixture in a vessel or still, while stirring, to a temperature of 140 (1; then turn off the heat and allow the evolution of ammonia to proceed (the temperature automatically rising) apply further heat after the rapid evolution of ammonia ceases, continuing the heat at a temperature of preferably 165 C.

for twelve to twenty-four hours; then raise,

anhydrous.

all combined; take 57 6 pounds of cresol and add to it the. molten resin just described. This provides a fusible phenolic condensation product containing about, one mol of hexa. to 15 mols of cresol, or 2 phenolic groups to each methylene group.

(6) Mix 1080 pounds of cresol '(2CH C H OH) and 93 pounds of hexamethylenetetramin (CH N heat the mixture in a vessel or still, while stirring, to a temperature of 140 (1; then turn off the heat and allow the evolution of ammonia to proceed (the temperature automatically-rising) apply further heat after the rapid evolution of ammonia ceases; continuing the heat at a temperature of preferably 165 C.

for twelve to twenty-fourhhours; then raise the temperature gradually through a period of from four to seven hours, reaching a temperature of about 215 C. and discontinue the heat after the methylene substance has all combined. This gives a fusible anhydrous phenolic condensation productcontaining about one mol of hexamethylenecresol, or about 2% to each methylene group.

A less desirable method of producing a fusible, substantially anhydrous phenolic condensation product adaptedfor use in the practice of the process is as follows:

Boil together a 40% solution of formaldehyde and cresol, taken in such proportions as to afford about 2.; phenolic groups to each methylene group, continuing the reaction until the formaldehyde is practically all combined with the phenol; eliminate the water, as by drawing off the supernatant liquid and concentrating the resinous mass. This gives a fusible, substantially anhydrous resin, containing about 2. phenolic groups to each methylene group. If the boiling operation is performed under conditions which will result in the loss of some of the formaldehyde, it is desirable to employ, in the first instance, somewhat more formaldehyde than corresponds with 2.; phenolic groups to each methylene group.

Having obtained by one of these methods, or a desired method, a fusible, substantially anhydrous phenoliccondensation product containing more than two phenolic groups to each methylene group, a molding compound adapted to a quick-molding operation and subsequent heat treatment after removal from the mold for hardening purposes may be produced by mixing with the fusible, substantially anhydrous resin a sufiicient quantity of fibrous filler to give the desired consistence, and a sufiicient quantity of a nonvolatile methylene substance which will unite anhydrously with the fusible resin to produce ahard and substantially infusible phenolic condensation product. For illustration, one may take the fusible resin in melted condition, preferably at a temperature of about 150 F., and add thereto enough hexamethylenetetramin to make the binder, as a whole, contain about one methylene group to each phenolic group, thus providing a potentially reactive binder, and this binder may be mixed with from two to three times its weight of asbestos, previously thoroughly mixed with a hydrocarbon solvent of high boiling-point. After the mixing operation, the molding compound may be subjected to a drying operation, and then mechanically disintegrated to produce a granulated molding product adapted to the quick-molding process. I

If desired, the granulated molding compound may' be rolled into sheets, which may be placed upon a steam-table and preparatorily warmed, and then balled up and introduced, in a warm condition, into the dies; or, the granulated moldmg compound may be -warmedand introduced in this forminto the'dies and subjected to a quick-molding operation. materials tends to the production of a finer "rained molded article, and to some extent hiay reduce the time of the curing operation stance, which is originally Such preparatory heating of the they acquire from operating upon the molding compound as preliminarily heated. It is advantageous, for instance, to subject the molding compound for a couple moments to a temperature of about 250 F., before introducing the compound into the mold.

It will be noted that the fusible anhydrous resin is produced, in the first instance, by completely combining the methylene subused with the phenol, by boiling the materials together. Thus, by. properly weighing the materials in the first instance, the boiling operation may be performed without danger of obtaining a condensation product in which the reaction has progressed beyond the stage where it is suitable for use in producing a cold molding compound. The fusible anhydrous phenolic condensation product may be shipped, in this condition, to manufacturers of molded products; and such manufacturers may readily perform the operation of mixing the fusible anhydrous phenolic condensation product with a sufficient quantity of hexamethylenetetramin to effect conversion to the final infusible state. and the requisite amount of fibrous filler to give the desired consistency to the molding mixture and desired qualities to the molded product.

By using a fusible, substantially anhydrous phenolic resin and a methylene substance which will combine therewith in an anhydrous reaction, after the quick-molding operation has been performed, the curing operation may be'readily performed without injury to the molded article, and a molded article will be produced which possesses high tensile strength, a high dielectric constant, and a body which has slight capability, if any, of water absorption. Any suitable phenolic body may be employed in produc ing the binder, such as phenol, or a homologue, cresols, or a mixture of cresols. Among the recognized equivalent phenolic bodies in the art may be mentioned phenol, the cresols,and the xylenols- The most desirable active methylene body for use in the process is the methylene-amin compound hexamethylenetetramin. Another instance of a non-volatile methylene-amin compound which is capable of being used in connection withthe fusible anhydrous resin combining therewith by an anhydrous reaction is hydrobenzamid. It may be stated, however, this latter substance is too expensive wat the present time to be economically employed in the process.

The foregoing detailed description has been given for clearness of understanding only, and no unnecessary limitation should that I quick-molding operation to form a be understood therefrom, but the appended claims should be construed as broadly as permissible, in view of the prior art.

'What I regard as new, and desire to secure by Letters Patent, is:

The process of producing a molded phenolic condensation product article, which comprises: initially mixing together a fibrous filler and a relatively small quan tity of a slowly-volatile solvent for a fusible phenolic condensation product; mixing together the filler thus impregnated and a binder comprising a substantially anhydrous phenolic condensation product correspondin with the reaction between a phenolic body and a methylene body in proportions affording at least two phenolic groups to each methylene group and a non-volatile methylene body in suflicient quantity to give to the molding mixture approximately one phenolic group to each methylene group; subjecting the molding compound bto a y; and subjecting the molded article, after removal from the mold, to prolonged heat treatment until a hard and substantially infusible body results.

2. The process of producing a molded phenolic condensation product article, which comprises: mixing together a fibrous filler and a slowly-volatile hydrocarbon solyent for a fusible phenolic condensation product; mixing with the filler thus impregnated a binder comprising a substantially anhydrous phenolic condensation product corresponding with the reaction between a phenolic body and a methylene body in proportions afi'ording at least two phenolic groups to each methylene group and hexamethylenetetramin in sufiicient quantity to give to the molding mixture approximately one methylene group to each phenolic group; subjecting the molding compound to a quick molding operation to form a body; and subjecting the-molded article, after removal from the mold, to prolonged heat treatment until a hard and substantially infusible body results.

3. The process of producing a molded phenolic condensation product article, which comprises: mixing filler and a relatively small quantity of a hydrocarbon solvent of high boiling-point; mixing the'filler thus impregnated and a binder comprising a substantially anhydrous .phenolic condensation product in which substantially all of the methylene substance employed in making such product has combined with the phenolic body,'such condensation product corresponding with the reaction between a phenolic body and a methylene body in proportions alfordin at least two phenolic groups to each methy one group, and hexamethylenetetramin in suifitogether a fibrous cient quantity to give to the molding mixture approximately one methylene group to a fibrous filler with a relatively small quan-' tity of hydrocarbon solvent of high boilingpoint; mixing together such impregnated filler and a binder comprising a fusible phenolic condensation product corresponding with thereaction between a phenolic body and a methylene body in proportions affording at least two phenolic groups to each methylene group and a non-volatile methylene body adapted to react anhydrously therewith, taken in suflicient quantity to give to the mately one methylene group to each phenolic group; drying and mechanicall treating the mixture to put it in suitab e form for use as a molding compound; preparatorily heating the molding compound; subjecting the preparatorily heated molding molding mixture approxi compound to a quick-molding operation to phenolic binder; and mixing the filler thus impregnated and a binder comprising unreacted hexamethylenetetramin and a fusible binder containing more than two phenolic groups to each methylene group vin said condensation product.

7 6. The process of producing a molding compound adapted for producing molded articles by a quick-molding operation followed by heat treatment, after removal ,of the article from the mold, which comprises: mixing a fibrous filler and a relatively small quantity of a slowly-volatile solvent for a phenolic binder; mixing the filler thus impregnated and a binder comprising unreacted hexamethylenetetramin and a fuiible phenolic condensation product in w ich substantially all of the methylene substance employed v1n making such condensation product is combined with the phenolic body phenolic condensation product, the

employed, the binder containing more than two phenolic groups to each methylene group in said condensation product, and drying anddisintegrating the mixture.

7. The process of producing a molding compound adapted for producing molded articles by a quick-molding operation followed by heat treatment, after removal of the article from the mold, which comprises: preparing a substantially anhydrous fusible phenolic condensation product containing more than two phenolic groups to each methylene group, the methylene substance employed in making such condensation product being substantially all combined' with the phenolic body employed; impregnating a fibrous filler with a hydrocarbon solvent having a high boiling-point; mixing with the filler thus impregnated the fusible phenolic condensation product and a sufficient quantity of hexamethylenetetramin to effect conversion of the binder to a hard and substantially infusible state; and v subjecting the compound to a drying and mechanical operation to place the same in desired condition for molding.

8. The process of producing a phenolic condensation product, which comprises: im-

pregnating a fibrous material with a light coal tar oil; mixing the impregnated material with a blnder comprising unreacted hexamethylenetetramin and a substantially .bined with the phenolic body employed, the

binder containing more than two phenolic groups to each methylene group of the phenolic condensation product and the hexamethylenetetramin being taken in sufficient quantity to effect conversion to a hard and substantially infusible state; and subjecting said fibrous mixture toa forming operation and heat treatment substantially as described, until a hard, resistant and substantially infusible body results.

CLARENCE A. NASH.